Method of Removing Sulfur Dioxide From A Flue Gas Stream

• US 20090241774A1
• Filed: 03/27/2009
• Published: 10/01/2009
• Est. Priority Date: 08/18/2005
• Status: Active Grant

• Current Assignee: Solvay Chemicals Incorporated (Solvac SA)
• Original Assignee: Solvay Chemicals Incorporated (Solvac SA)
• Inventors: MAZIUK, John JR.
• Granted Patent: US 7,854,911 B2
• Time in Patent Office: Days
• US Class Current: 95/58
• CPC Class Codes: B01D 53/508 by treating the gases with solids

Abstract

A method of removing SO_x from a flue gas stream including SO_x includes providing a source of trona and injecting the trona as a dry sorbent into the flue gas stream. The temperature of the flue gas is at an elevated temperature greater than 400° F., preferably between about 600° F. and about 900° F. The trona is maintained in contact with the flue gas for a time sufficient to react a portion of the trona with a portion of the SO_x to reduce the concentration of the SO₂ and/or SO₃ in the flue gas stream.

Claims

1. A method of removing SO₂ from a flue gas stream comprising SO₂, comprising:

providing a source of trona;

injecting the trona into the flue gas stream, wherein the temperature of the flue gas is between about 600°

F. and about 900°

F.; and

maintaining the trona in contact with the flue gas for a time sufficient to react a portion of the trona with a portion of the SO₂ to reduce the concentration of the SO₂ in the flue gas stream.

2. The method of claim 1 wherein the mean particle size of the trona is less than about 40 micron.

3. The method of claim 1 wherein the mean particle size of the trona is between about 10 micron and about 40 micron.

4. The method of claim 1 wherein the mean particle size of the trona is between about 24 micron and about 28 micron.

5. The method of claim 1 wherein the temperature of the flue gas is greater than about 630°

F.

6. The method of claim 1 wherein the temperature of the flue gas is greater than about 700°

F.

7. The method of claim 1 wherein the temperature of the flue gas is less than about 800°

F.

8. The method of claim 1 wherein the temperature of the flue gas is less than about 750°

F.

9. The method of claim 1 wherein the temperature of the flue gas is between about 700°

F. and about 750°

F.

10. The method of claim 1 wherein the trona is injected at a rate with respect to the flow rate of the SO₂ to provide a normalized stoichiometric ratio of sodium to sulfur of between about 1.0 and 1.5.

11. The method of claim 1 wherein the trona is injected as a dry material.

12. The method of claim 1 further comprising milling the trona to a desired mean particle size at a location proximate the flue gas stream.

13. The method of claim 1 further comprising collecting a reaction product of the trona and the SO₂ in an electrostatic precipitator.

14. The method of claim 1 wherein the flue gas stream further comprises SO₃, further comprising maintaining the trona in contact with the flue gas for a time sufficient to react a portion of the trona with a portion of the SO₃ to reduce the concentration of the SO₃ in the flue gas stream.

15. A method of removing SO₃ from a flue gas stream comprising SO₃, comprising:

providing a source of trona;

injecting the trona as a dry sorbent material into the flue gas stream, wherein the flue gas is at an elevated temperature greater than 400°

F.; and

maintaining the trona in contact with the flue gas for a time sufficient to react a portion of the trona with a portion of the SO₃ to reduce the concentration of the SO₃ in the flue gas stream.

16. The method of claim 15 wherein the mean particle size of the trona is less than about 40.

17. The method of claim 15 wherein the mean particle size of the trona is between about 10 micron and about 40 micron.

18. The method of claim 15 wherein the mean particle size of the trona is between about 24 micron and about 28 micron.

19. The method of claim 15 wherein the temperature of the flue gas is between about 600°

F. and about 900°

F.

20. The method of claim 15 wherein the temperature of the flue gas is greater than about 630°

F.

21. The method of claim 15 wherein the temperature of the flue gas is greater than about 700°

F.

22. The method of claim 15 wherein the temperature of the flue gas is less than about 800°

F.

23. The method of claim 15 wherein the temperature of the flue gas is less than about 750°

F.

24. The method of claim 15 wherein the temperature of the flue gas is between about 700°

F. and about 750°

F.

25. The method of claim 15 wherein the trona is injected at a rate with respect to the flow rate of the SO₃ to provide a normalized stoichiometric ratio of sodium to sulfur of between about 1.0 and 1.5.

26. The method of claim 15 further comprising milling the trona to a desired mean particle size at a location proximate the flue gas stream.

27. The method of claim 15 further comprising collecting a reaction product of the trona and the SO₃ in an electrostatic precipitator.